EP1025160B1 - Zusammensetzung modifizierter stärke zum entfernen von teilchen aus wässrigen dispersionen - Google Patents

Zusammensetzung modifizierter stärke zum entfernen von teilchen aus wässrigen dispersionen Download PDF

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Publication number
EP1025160B1
EP1025160B1 EP98953929A EP98953929A EP1025160B1 EP 1025160 B1 EP1025160 B1 EP 1025160B1 EP 98953929 A EP98953929 A EP 98953929A EP 98953929 A EP98953929 A EP 98953929A EP 1025160 B1 EP1025160 B1 EP 1025160B1
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EP
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Prior art keywords
starch
pam
cationic
cooking
polyacrylamide
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Expired - Lifetime
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EP98953929A
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English (en)
French (fr)
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EP1025160A1 (de
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Robert Harvey Moffett
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University of Maine System
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University of Maine System
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/46—Polyesters chemically modified by esterification
    • C08G63/48—Polyesters chemically modified by esterification by unsaturated higher fatty oils or their acids; by resin acids
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B31/00—Preparation of derivatives of starch
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L3/00—Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
    • C08L3/04—Starch derivatives, e.g. crosslinked derivatives
    • C08L3/08—Ethers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24—Polysaccharides
    • D21H17/28—Starch
    • D21H17/29—Starch cationic
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
    • C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
    • D21H17/375—Poly(meth)acrylamide
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/42—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
    • D21H17/66—Salts, e.g. alums
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/06—Paper forming aids
    • D21H21/10—Retention agents or drainage improvers

Definitions

  • This invention relates to compositions obtained by cooking a cationic or amphoteric starch and a cationic, nonionic, or amphoteric polyacrylamide.
  • the resulting modified starch compositions have general utility as a clarifying aid for removing solids from an aqueous dispersion, and have special utility as a retention aid in the manufacture of paper.
  • Paper production involves the formation and dewatering of a web primarily composed of cellulose fibers and inorganic filler.
  • the web is formed by spreading an aqueous suspension containing the cellulose fibers and inorganic filler over a wire or net, and then removing water to form a fiber web or sheet.
  • the aqueous suspension is referred to as "paper furnish” in the trade, and the removed water is referred to as "white water.”
  • Cationic starches frequently are used for this purpose, particularly the relatively expensive cationic potato and waxy maize starches. Less expensive cationic corn starch has been used, but it generally does not provide adequate fines retention and wet-end drainage.
  • amphoteric and cationic starches exhibit improved performance as a retention additive in the manufacture of paper if the starches are cooked with a cationic, nonionic, or amphoteric polyacrylamide.
  • the invention provides a modified starch prepared by cooking an amphoteric starch or cationic starch having a degree of substitution between 0.01 to 0.2 with at least one polyacrylamide having a molecular weight of at least 500,000 selected from the group consisting of a nonionic polyacrylamide, an amphoteric polyacrylamide, and a cationic polyacrylamide having a degree of substitution between 1% and 80% by weight, said cooking being at a temperature of at least about 60°C in an aqueous solution having a pH above about 7.0, wherein the weight ratio of starch to polyacrylamide is greater than 5 to 1, for a time effective to modify said starch. While the modified starch has particular utility in the manufacture of paper, it also has general utility for removing solids from aqueous suspensions.
  • modified starches improve fines retention and wet-end drainage in the paper-making process, while allowing the selection of less expensive or reduced amounts of certain additives. More specifically, it has been found that cationic or amphoteric starches, when cooked with a cationic, nonionic, or amphoteric polyacrylamide, improve fines retention over that achieved by separately adding the starch and polyacrylamide during the paper-making process.
  • the cationic starch may be any of those previously used in papermaking.
  • the cationic starch may be derived from any of the common starch producing materials such as corn starch, potato starch, waxy maize starch and wheat starch. Cationization is achieved by any of the commercially known procedures, such as the addition of 3-chloro-2-hydroxypropyltrimethylammonium chloride to obtain cationic starches with various degrees of nitrogen substitution.
  • the degree of cationic substitution on the starches can range from 0.01 to 0.2, preferably between 0.02 and 0.15.
  • Naturally occurring amphoteric starches, such as potato starch, or synthetic amphoteric starches also may be selected.
  • the PAM is nonionic, amphoteric, or preferably cationic, having a molecular weight of at least 500,000, preferably at least 1,000,000.
  • the cationic and amphoteric PAM may have a degree of cationic substitution by weight from 1% to 80%, preferably from 10% to 40%.
  • degree of substitution it is meant that the polymers contain randomly repeating monomer units containing chemical functionality which, when dissolved in water, become cationically charged. These monomer units include, but are not limited to, groups such as amino groups.
  • the PAM may be a solid, powder form, micro-bead form, a water-in-oil emulsion or any other commercially known form. Suitable PAM can be obtained from Allied Colloids, Suffolk VA, and from Nalco, Naperville IL, as well as other sources.
  • the starch and PAM may be dry blended together or blended as a slurry or slurries in water before being cooked, or they may be blended during the starch cooking process. Rather than blending dry or slurried PAM, the PAM may instead be prehydrated before being blended and cooked with the starch. Rather than blending dry or slurried starch, the starch may instead be cooked, blended with the PAM, and then recooked.
  • Cooking conveniently is accomplished using a starch cooker at the paper mill.
  • a batch cooker or continuous cooker such as a jet cooker, may be selected.
  • Continuous jet cooking typically is conducted at temperatures from 80 to 130°C at 1 atmosphere or higher pressure.
  • the solids content during cooking generally is less than 15%, but higher solids concentrations may be used if adequate mixing can be accomplished.
  • Selected cooking times and temperatures varies with the composition and equipment. Cooking conditions must be sufficient to gelatinize the starch and for the PAM to at least partially hydrate and react with the starch.
  • the cooking or heating temperatures is at least about 60°C, preferably at least 65°C, and most preferably at least 80°C to 100°C. For example, advantages of the invention have been observed at cooking temperatures as low as 60°C. Temperatures above 100°C may be selected if decomposition of the starch and PAM is prevented.
  • batch cooking can be selected in practicing the invention, at pressures greater than one atmosphere, to employ a cooking temperature higher than 100°C and as high as 130°C, or higher.
  • the selected cooking time typically will be in the range of a few minutes to less than an hour. Longer cooking times generally are required for lower cooking temperatures.
  • cationic or nonionic PAM When using cationic or nonionic PAM, best results arc obtained if the starch/PAM mixture is cooked at a pH above 7, although some improvement in ash retention is also found at a pH below 7.
  • the preferred cooking pH for either cationic or nonionic PAM and starch is from 8 to 10.5. pH is not critical when an amphoteric PAM is selected, but typically will be in the range of 3 to 11.
  • Cooking pH may be adjusted with conventional acids, bases, or salts.
  • Use of alkaline aluminum compounds, such a sodium and potassium aluminate, have been found to be particularly useful for this purpose as these compounds also boost retention performance, as illustrated in Example 6.
  • retention performance is thereby improved even in acid paper furnishes.
  • inclusion of the alkaline aluminum compound in the cooking solution results in a modified starch that permits us of a non-aluminized microparticulate retention aid in acidic paper furnishes, to further improve retention performance, whereas these non-alumized retention aids typically do not perform well in acidic paper furnishes.
  • the weight ratio of PAM to starch will vary with the selected ingredients, and the extent to which improvements are desired in fines retention and wet end drainage. For example, it has been-found that poor-performing corn starch may be improved to the extent that it is equal or superior to the more expensive potato starch by cooking the corn starch with as little as 1% PAM, by weight Typically, the selected weight ratio of starch to PAM will be greater than 5 to 1, preferably greater than 10 to 1. The amount of PAM added to the starch should be limited below that which would cause the starch to precipitate, which will vary with the ingredients and cooking process that is selected.
  • the cooked starch/PAM composition may be added to any suitable paper furnish as a retention aid to improve fines retention and wet end drainage.
  • the paper furnish may contain a variety of wood pulp and inorganic fillers, and typically has a pH of 4 to 10.
  • bleached kraft pulp, thermomechanical, chemical-thermomechanical and groundwood pulps may be used together with clays, precipitated or ground calcium carbonate, titanium dioxide and other inorganic fillers if desired.
  • Such fillers typically arc used at the 15% to 20% loading level, as a weight percent of the total paper weight, but may reach levels as high as 30%, or higher, for some specialty applications.
  • the paper furnish also contains an anionic inorganic colloid, as is conventional in the paper-making industry.
  • the furnish may contain, for example, montmorillonite, bentonite, silica sols, aluminum modified silica sols, aluminum silicate sols, polysilicic acid, polysilicate microgels and polyaluminosilicate microgels, separately or in combination.
  • the paper furnish also may contain other typical additives, such as size, aluminum compounds (alum, aluminates, polyaluminum chlorides, etc.), cationic polymers (retention aids and flocculents), anionic polymers, and/or separate additions of starch.
  • Aluminum compounds in particular have been found to boost retention performance of the cooked starch/PAM compositions. While the above ingredients may be added in any order with good results, the preferred order of addition is to add the alumina compound first, the cooked/PAM of this invention next, and then an inorganic anionic colloid.
  • compositions also have utility as clarifying aids to remove solids from aqueous suspensions.
  • the performance of the test solutions was measured as retention aids in a 5 gram/liter paper furnish composed of 35% bleached kraft hardwood, 35% bleached kraft softwood, and 30% precipitated calcium carbonate (PCC).
  • the furnish pH was 8.0.
  • the furnish was mixed in Britt Jar equipped with a 50R screen (100 mesh) at 750 RPM. Ash retention's were determined from the white water sample by following Tappi Standard T-261.
  • a dry blend was prepared by mixing 3.0 grams of Stalok 300 cationic corn starch from Staley Starch with 0.04 grams of cationic PAM "A" having a molecular weight of about 4,000,000 and a degree of substitution of 22 wt.%. This blend was added to 497 grams of deionized water and the pH adjusted to 8.5 using sodium hydroxide. The solution was heated on a hot plate stirrer for 30 minutes and began to boil at about 15 minutes into the cooking cycle. After cooking the solution was removed from the hot plate and allowed to cool. The solution was reweighed and any water which evaporated was replaced.
  • a second dry blend was prepared by mixing 3.0 grams of BMB-40 cationic potato starch from Akzo Nobel with 0.04 grams of PAM "A". To this blend was added 497 grams deionized water and the pH was adjusted to 8.5 and cooked following the method described above.
  • samples of Stalok 300 corn starch and BMB-40 potato starch were prepared as 0.5 wt % solutions following the cooking procedure above. The pH of these starch solutions was not adjusted. A 0.125 wt.% sample of PAM "A” was separately prepared by adding 1 gram of PAM "A” to 799 grams of deionized water and mixing the resulting solution for 1 hour.
  • Starch and PAM were separately added to the furnish at a dose rate of 15 lb/ton (7.5 kg/tonne) and 0.25 lb/ton (0.125 kg/tonne) respectively.
  • polyaluminosilicate microgel solution prepared following U.S. 5,482,693 was added to the furnish in some tests.
  • the order of chemical addition was: Time (sec) Step 00 Start mixer 15 Add starch; add PAM 30 Add PAS 45 Open Britt Jar drain valve 50 Begin collecting white water 80 Stop collection white water
  • This example demonstrates the need to cook the cationic starch and cationic PAM together rather than simply mixing them at lower temperatures.
  • Sample A was prepared by mixing 3.0 grams of Stalok 300 with 497 grams of deionized water and adjusting the pH to 8.5. The solution was cooked using the cooking procedure described in Example 1. After the sample had cooled to 35°C, 0.04 grams of PAM "A" was added and the resulting solution was mixed for 1 hour before testing.
  • Sample B was prepared by mixing 3.0 grams of Stalok 300 with 497 grams of deionized water and adjusting the pH to 8.5. The solution was cooked using the cooking procedure described in Example 1. After the sample had cooled to 95°C, 0.04 grams of PAM "A" was added and the resulting solution was mixed for 1 hour before testing.
  • Sample C was prepared by blending 3.0 grams of Stalok 300 with 0.04 grams of PAM "A”, then adding 497 grams of deionized water and adjusting the pH to 8.5. The solution was cooked using the cooking procedure described in Example 1.
  • Table 2 shows the ash retention results.
  • the pH of the starch solution or starch/PAM solution before cooking is labeled as "a:pH”.
  • the pH after cooking was also measured, and is labeled as "b:pH”.
  • This example demonstrates that cationic starch blended and cooked with prehydrated cationic PAM at pH 8.5 also improves retention.
  • a sample of 0.125% cationic PAM was prepared by adding 1.0 grams of PAM "B” to 799 grams of deionized water. The solution was allowed to hydrate for 1 hour. Then 33.3 grams of this 0.125% PAM solution was mixed with 464 grams of deionized water and 3.0 grams of Stalok 300. The pH was then adjusted to 8.5 and the solution was cooked following the cooking procedure described in Example 1.
  • a second starch/PAM blend was prepared by dry blending 0.04 grams of PAM "B” with 3 grams of Stalok 300 and then adding the dry blend to 497 grams of deionized water. The pH was adjusted to 8.5 and cooked following the procedure described in Example 1.
  • a dry blend was prepared by mixing 3.0 grams of Stalok 300 cationic corn starch from Staley Starch with 0.04 grams of cationic PAM "A". To this blend was added 497 grams of deionized water. The pH was adjusted to 8.6. The solution was heated on a hot plate stirrer for 30 minutes and began to boil about 15 minutes into the cooking cycle. After cooking the solution was reweighed and any water which evaporated was replaced. The final pH of the solution was 7.1.
  • This example demonstrates how using an alkaline aluminum compound to adjust the cationic starch/cationic PAM to pH above 7 before cooking boosts the blend's performance as a retention aid.
  • Dry blends were prepared by mixing 3.0 grams of Stalok 300 cationic corn starch with 0.04 grams of PAM "B" and various amounts of sodium aluminate as listed for Samples D through G in Table 7. To these blends was added 497 grams of deionized water. The pH in the blend containing no sodium aluminate was adjusted to 8.5. The pH in the blends containing sodium aluminate was measured but not adjusted and is labeled as "a:pH". The solution was heated on a hot plate stirrer for 30 minutes and began to boil about 15 minutes into the cooking cycle. After cooking, the solution was reweighed and any water which had evaporated was replaced. The pH of the solution was again measured and is labeled as "b:pH”.
  • This example demonstrates how cooking cationic starch and nonionic PAM together at pH 10 yields better retention than adding the same two chemicals separately but simultaneously to the paper furnish.
  • a dry blend was prepared by mixing 3.0 grams of Stalok 300 cationic corn starch from Staley Starch with 0.04 grams of nonionic PAM "D", having a molecular weight of about 14,000,000. To this blend was added 497 grams of deionized water. The pH was adjusted to 10.1. The solution was heated on a hot plate stirrer for 30 minutes and began to boil about 15 minutes into the cooking cycle. After cooking the solution was reweighed and any water which evaporated was replaced. The final pH of the solution was 9.9.
  • Stalok 300 As a comparison, a sample of Stalok 300 was prepared as a 0.5 wt.% solution following the procedure above. The solution pH was found to be 7.5 and was not adjusted.
  • a 0.125 wt.% solution of PAM "D” was prepared by adding 1 gram of PAM “D” to 799 grams of deionized water and mixing the resulting solution for 1 hour. The solution pH was found to be 4.4 and was not adjusted.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Colloid Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Claims (7)

  1. Modifizierte Stärke, erhalten durch Erhitzen mindestens einer amphoteren Stärke oder kationischen Stärke, die einen Substitutionsgrad zwischen 0,01 bis 0,2 aufweist, mit mindestens einem Polyacrylamid, das ein Molekulargewicht von mindestens 500 000 aufweist und das ausgewählt ist aus der Gruppe bestehend aus einem nicht-ionischen Polyacrylamid, einem amphoteren Polyacrylamid und einem kationischen Polyacrylamid mit einem Substitutionsgrad zwischen 1 Gew.-% und 80 Gew.-%, wobei das Erhitzen bei einer Temperatur von mindestens 60 °C in einer wäßrigen Lösung mit einem pH über 7,0 durchgeführt wird und wobei das Gewichtsverhältnis von Stärke zu Polyacrylamid größer als 5 zu 1 ist, über einen Zeitraum, der ausreicht, daß die Stärke verkleistert und daß das Polyacrylamid die Stärke zumindest teilweise hydratisiert und mit ihr reagiert.
  2. Modifizierte Stärke nach Anspruch 1, dadurch gekennzeichnet, daß eine kationische Stärke mit einem kationischen Polyacrylamid erhitzt wurde.
  3. Modifizierte Stärke nach Anspruch 2, dadurch gekennzeichnet, daß das Gewichtsverhältnis von kationischer Stärke zu kationischem Polyamid größer als 10 zu 1 ist.
  4. Modifizierte Stärke nach einem der Ansprüche 1 oder 2, dadurch gekennzeichnet, daß die Stärke ausgewählt ist aus der Gruppe bestehend aus Maisstärke, Kartoffelstärke und Wachsmaisstärke.
  5. Modifizierte Stärke nach einem der Ansprüche 1 oder 2, dadurch gekennzeichnet, daß eine alkalische Aluminiumverbindung in der erhitzten Lösung anwesend ist.
  6. Modifizierte Stärke nach einem der Ansprüche 1 bis 5, dadurch gekennzeichnet, daß das Erhitzen bei einer Temperatur von mindestens 80 °C durchgeführt wird.
  7. Papiermaterial, enthaltend die modifizierte Stärke nach einem der Ansprüche 1 bis 6.
EP98953929A 1997-10-30 1998-10-23 Zusammensetzung modifizierter stärke zum entfernen von teilchen aus wässrigen dispersionen Expired - Lifetime EP1025160B1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US08/960,648 US5859128A (en) 1997-10-30 1997-10-30 Modified cationic starch composition for removing particles from aqueous dispersions
US960648 1997-10-30
PCT/US1998/022489 WO1999023156A1 (en) 1997-10-30 1998-10-23 Modified starch composition for removing particles from aqueous dispersions

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EP1025160A1 EP1025160A1 (de) 2000-08-09
EP1025160B1 true EP1025160B1 (de) 2002-09-04

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US (2) US5859128A (de)
EP (1) EP1025160B1 (de)
JP (1) JP2001521965A (de)
KR (1) KR100553306B1 (de)
CN (1) CN1103795C (de)
AT (1) ATE223459T1 (de)
AU (1) AU738445B2 (de)
BR (1) BR9812988A (de)
CA (1) CA2305471C (de)
CZ (1) CZ293483B6 (de)
DE (1) DE69807724T2 (de)
EA (1) EA002007B1 (de)
ES (1) ES2182369T3 (de)
HU (1) HUP0004163A3 (de)
ID (1) ID24670A (de)
NO (1) NO20002179L (de)
NZ (1) NZ504094A (de)
PL (1) PL191632B1 (de)
PT (1) PT1025160E (de)
SK (1) SK6032000A3 (de)
WO (1) WO1999023156A1 (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1971589B (zh) * 2005-11-22 2010-12-08 香港理工大学 无源射频标签反假冒的系统和方法

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5859128A (en) * 1997-10-30 1999-01-12 E. I. Du Pont De Nemours And Company Modified cationic starch composition for removing particles from aqueous dispersions
US6033525A (en) * 1997-10-30 2000-03-07 Moffett; Robert Harvey Modified cationic starch composition for removing particles from aqueous dispersions
DE19832241A1 (de) * 1998-07-17 2000-01-27 Stockhausen Chem Fab Gmbh Verwendung von modifizierten Stärkeprodukten als Retentionsmittel bei der Papierherstellung
US6441315B1 (en) * 1998-11-10 2002-08-27 Formfactor, Inc. Contact structures with blades having a wiping motion
US6217709B1 (en) 1998-11-23 2001-04-17 Hercules Incorporated Cationic starch/cationic galactomannan gum blends as strength and drainage aids
ES2208309T3 (es) * 1999-04-01 2004-06-16 Basf Aktiengesellschaft Modificacion de almidon con polimeros cationicos y empleo de almidones modificados como agente de solidificacion en seco para papel.
CN1377436A (zh) * 1999-10-19 2002-10-30 韦尔豪泽公司 阳离子改性的多糖
FI113968B (fi) * 2001-05-23 2004-07-15 Raisio Chem Oy Kationisella polysakkaridilla stabiloitu liuospolymeeri
US6699363B2 (en) 2001-11-13 2004-03-02 E. I. Du Pont De Nemours And Company Modified starch and process therefor
US7022194B2 (en) * 2002-07-24 2006-04-04 Enchem Chemical Products, Inc Method of treating a paint booth dry filter
JP4650605B2 (ja) * 2003-01-17 2011-03-16 靖彦 大西 陽イオン性多糖類共重合体ベクタ−
WO2004076551A1 (en) * 2003-02-27 2004-09-10 The University Of Maine Board Of Trustees Starch compositions and methods of making starch compositions
EP1641430A2 (de) * 2003-07-01 2006-04-05 The University of Maine Board of Trustees Gelierte stärkezusammensetzungen und verfahren zur herstellung von gelierten stärkezusammensetzungen
US8147979B2 (en) 2005-07-01 2012-04-03 Akzo Nobel Coatings International B.V. Adhesive system and method
US7273836B2 (en) * 2005-09-19 2007-09-25 Enchem Chemicals Products, Inc. Paint detackifier and detoxifier
JP2009520849A (ja) * 2005-12-22 2009-05-28 クラリアント インターナショナル リミティド 紙およびボードの生産用乾燥強度系
EP2032656B2 (de) * 2006-06-23 2016-05-25 Akzo Nobel Coatings International B.V. Klebstoffsystem und verfahren zur herstellung eines auf holz basierenden produkts
US8048257B2 (en) * 2006-06-23 2011-11-01 Akzo Nobel Coating International B.V. Adhesive system and method of producing a wood based product
US20090317651A1 (en) * 2006-06-23 2009-12-24 Akzo Nobel Coatings International B.V. Adhesive system and method of producing a wood based product
CN100572434C (zh) * 2007-06-05 2009-12-23 内江市春江纸业有限公司 一种改性淀粉组合物的制备方法
CN101333297B (zh) * 2007-06-26 2011-06-29 财团法人工业技术研究院 有机/无机杂化材料及其形成方法
FI124234B (en) * 2012-03-23 2014-05-15 Kemira Oyj Process for dissolving cationic starch, papermaking agent and its use
FI125712B (en) * 2012-11-13 2016-01-15 Kemira Oyj Paper-making material and its use
JP6903694B2 (ja) * 2016-07-01 2021-07-14 エコラブ ユーエスエイ インク 低塩化物塗料脱粘着剤

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1177512A (en) * 1966-04-15 1970-01-14 Nalco Chemical Co Improved Papermaking Process
US4066495A (en) * 1974-06-26 1978-01-03 Anheuser-Busch, Incorporated Method of making paper containing cationic starch and an anionic retention aid
DE2821830A1 (de) * 1978-05-19 1979-11-22 Basf Ag Verfahren zur oberflaechenleimung von papier
SE432951B (sv) * 1980-05-28 1984-04-30 Eka Ab Pappersprodukt innehallande cellulosafibrer och ett bindemedelssystem som omfattar kolloidal kiselsyra och katjonisk sterkelse samt forfarande for framstellning av pappersprodukten
JPS60126398A (ja) * 1983-12-13 1985-07-05 株式会社協立有機工業研究所 紙の乾燥強度を向上させる抄紙方法
US4643801A (en) * 1986-02-24 1987-02-17 Nalco Chemical Company Papermaking aid
JP2525602B2 (ja) * 1987-05-02 1996-08-21 星光化学工業株式会社 製紙方法
US5176891A (en) * 1988-01-13 1993-01-05 Eka Chemicals, Inc. Polyaluminosilicate process
JP2720460B2 (ja) * 1988-06-27 1998-03-04 日産化学工業株式会社 製紙方法
US4954220A (en) * 1988-09-16 1990-09-04 E. I. Du Pont De Nemours And Company Polysilicate microgels as retention/drainage aids in papermaking
SE8903752D0 (sv) * 1989-11-09 1989-11-09 Eka Nobel Ab Foerfarande foer framstaellning av papper
US5178730A (en) * 1990-06-12 1993-01-12 Delta Chemicals Paper making
FR2682132B1 (fr) * 1991-10-08 1993-12-10 Zschimmer Schwarz France Procede pour ameliorer les proprietes de resistance du papier, notamment a l'eclatement, et papier ainsi obtenu.
JPH06166986A (ja) * 1992-11-30 1994-06-14 Seiko Kagaku Kogyo Co Ltd 製紙方法
US5482693A (en) * 1994-03-14 1996-01-09 E. I. Du Pont De Nemours And Company Process for preparing water soluble polyaluminosilicates
US5482595A (en) * 1994-03-22 1996-01-09 Betz Paperchem, Inc. Method for improving retention and drainage characteristics in alkaline papermaking
US5859128A (en) * 1997-10-30 1999-01-12 E. I. Du Pont De Nemours And Company Modified cationic starch composition for removing particles from aqueous dispersions

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1971589B (zh) * 2005-11-22 2010-12-08 香港理工大学 无源射频标签反假冒的系统和方法

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DE69807724D1 (de) 2002-10-10
NO20002179D0 (no) 2000-04-27
ES2182369T3 (es) 2003-03-01
CA2305471A1 (en) 1999-05-14
CN1278283A (zh) 2000-12-27
SK6032000A3 (en) 2001-02-12
EA002007B1 (ru) 2001-10-22
KR20010031652A (ko) 2001-04-16
US6048929A (en) 2000-04-11
JP2001521965A (ja) 2001-11-13
NZ504094A (en) 2001-06-29
PL191632B1 (pl) 2006-06-30
EA200000473A1 (ru) 2000-10-30
CN1103795C (zh) 2003-03-26
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PL340419A1 (en) 2001-02-12
CZ293483B6 (cs) 2004-05-12
PT1025160E (pt) 2003-01-31
HUP0004163A3 (en) 2001-11-28
AU738445B2 (en) 2001-09-20
WO1999023156A1 (en) 1999-05-14
BR9812988A (pt) 2000-08-08
ATE223459T1 (de) 2002-09-15
KR100553306B1 (ko) 2006-02-20
US5859128A (en) 1999-01-12
DE69807724T2 (de) 2003-05-08
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CA2305471C (en) 2008-01-08
ID24670A (id) 2000-07-27

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